TW546459B - Evaporator and refrigerator - Google Patents
Evaporator and refrigerator Download PDFInfo
- Publication number
- TW546459B TW546459B TW090118199A TW90118199A TW546459B TW 546459 B TW546459 B TW 546459B TW 090118199 A TW090118199 A TW 090118199A TW 90118199 A TW90118199 A TW 90118199A TW 546459 B TW546459 B TW 546459B
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- TW
- Taiwan
- Prior art keywords
- heat transfer
- refrigerant
- tube
- evaporator
- transfer tubes
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
- F28D7/163—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/02—Details of evaporators
- F25B2339/024—Evaporators with refrigerant in a vessel in which is situated a heat exchanger
- F25B2339/0242—Evaporators with refrigerant in a vessel in which is situated a heat exchanger having tubular elements
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2500/00—Problems to be solved
- F25B2500/01—Geometry problems, e.g. for reducing size
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S165/00—Heat exchange
- Y10S165/91—Tube pattern
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Geometry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
546459546459
發明背景 發明之技術領域 本七月係在提供一種蒸發器,該蒸發器係使被冷卻物(例 如水 '海水等等)與冷媒之間進行熱交換而冷卻被冷卻物; 以及提供一種具備有該蒸發器的冷凍機。 相關技術之描述 例如在像大厦的大建築物裡,把用冷;東機冷卻的冷卻水 通過敷設在建築物内的配管使其循環,使與各空間的空氣 熱交換而達到冷氣效果。 將具有冷東機的蒸發器的一個例子表示於圖1〇。蒸發器 的構造為:在冷媒被引進的圓筒形的容器α,流通冷水的 多數傳熱管2成交錯狀地成捆被配置。傳熱管2與連通於冷 水入口 3的去程傳熱管及連通於冷水彳口4相程傳熱管分 開,從冷水入口 3流入的冷水由容器丨裏的去程傳熱管到達 通水室(圖省略)折回在再通過容器丨裏的去程傳熱管從冷水 入口 4流出。在此過程’冷水在與被導入容器i的冷媒之間 進行熱交換而被冷卻;另一方面’冷媒被冷水奪去熱量, 沸騰而汽化。 不過,因為先前的蒸發器的構造為將多數的傳熱管拥成 一把,所以在位於容器的下部的傳熱管的周圍彿騰的冷媒 變成氣泡;因為纏繞位於其上的傳熱管由液體裡浮上,所 以液態的冷媒在上部的傳熱管的周圍,有不被充份供應的 傾向。因此,有個問題,就是特別是配置在成捆的中央。(相 當在芯的部分)附近的傳熱管熱傳達效率比配置在周圍的傳BACKGROUND OF THE INVENTION Field of the Invention The present invention is to provide an evaporator which cools the object to be cooled by performing heat exchange between the object to be cooled (for example, water, seawater, etc.) and a refrigerant; and The evaporator of the freezer. Description of related technology For example, in a large building like a building, the cooling water cooled by the machine is cooled by the pipes laid in the building to circulate the heat, so as to exchange heat with the air in each space to achieve the cooling effect. An example of an evaporator having a cold engine is shown in FIG. 10. The structure of the evaporator is such that a plurality of heat transfer tubes 2 through which cold water flows are arranged in a staggered bundle in a cylindrical container? Into which a refrigerant is introduced. The heat transfer tube 2 is separated from the outbound heat transfer tube connected to the cold water inlet 3 and the four-phase heat transfer tube connected to the cold water inlet 3. The cold water flowing from the cold water inlet 3 reaches the water through the outbound heat transfer tube in the container The chamber (not shown) is folded back and then flows out of the cold water inlet 4 through the outbound heat transfer tube in the container. In this process, the cold water is cooled by exchanging heat with the refrigerant introduced into the container i; on the other hand, the cold water is deprived of heat by the cold water and boiled and vaporized. However, because the previous evaporator was constructed to hold most of the heat transfer tubes, the refrigerant that turned around around the heat transfer tubes located in the lower part of the container became air bubbles; because the heat transfer tubes wound on it were made of liquid It floats inside, so the liquid refrigerant tends to be insufficiently supplied around the upper heat transfer tube. Therefore, there is a problem, especially in the center of the bundle. (Relatively in the core part) The heat transfer efficiency of the heat transfer tubes near
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-4- 546459 五、發明説明(2 A7 B7-4- 546459 V. Description of the invention (2 A7 B7
熱管來得低。 發明所欲解決之課題 '本發明之目的係#於上述之情事’卩改善在容器中海騰 冷媒的氣泡的脫離,來提高蒸發器的傳達效率,更進一步 依此提供高效率高的冷凍機。 V 解決上述課題的手段,採用如下構成的蒸發器及冷陳 :。也就是說有關本發明的蒸發器,其係在冷媒被引進的 容器裏,流通被冷卻物的多數傳熱管成捆地被配置而構 成,在上述冷媒與上述被冷卻物之間進行熱交換’冷卻哼 被冷卻物’同時將上述冷媒汽化;該上述傳熱管被:成; 數的管群,該管群之間彼此分離地被配置。 至於此瘵發器,係由於將傳熱管被分成複數的管群,該 管群之間彼此分離地被配置,因而位於比較下方的傳熱管 的周圍所產生的氣泡,由管群與管群之間脫離浮起,存| 於管群内的氣泡因而減少。因此,對配置在管群中央附近 的傳熱管影響的氣泡就變少,而能夠抑制熱傳達效率的降 低。 再者,雖然被引進容器内的液狀冷媒產生流動,但是由 於官群之間是彼此分離地被配置,冷媒變成容易流動。因 此’能夠促進冷媒液與傳熱管的接觸,而達到熱傳達效率 的提高。 此外,在上述的此蒸發器,其複數的管群也可以交錯狀 地被配置。 一種洛發器’其構造為液狀的冷媒由容器的下方被引 -5-The heat pipe came low. Problem to be Solved by the Invention 'The purpose of the present invention is #in the above-mentioned circumstances', to improve the release of air bubbles from the refrigerant in the container, to improve the transmission efficiency of the evaporator, and to provide a highly efficient refrigerator. V Means to solve the above-mentioned problems, the evaporator and the cold aging are adopted as follows:. In other words, the evaporator of the present invention is configured in a container in which a refrigerant is introduced, and a plurality of heat transfer tubes that circulate the object to be cooled are arranged in a bundle, and heat exchange is performed between the refrigerant and the object to be cooled. The 'cooling humic object' simultaneously vaporizes the above-mentioned refrigerant; the above-mentioned heat transfer tube is formed into; and a number of tube groups are arranged separately from each other. As for this hairspreader, the heat transfer tubes are divided into a plurality of tube groups, and the tube groups are arranged separately from each other. Therefore, the air bubbles generated around the lower heat transfer tubes are compared by the tube groups and the tubes. The separation between the clusters floats, and the air bubbles in the clusters are reduced. Therefore, the number of bubbles affecting the heat transfer tubes arranged near the center of the tube group is reduced, and a decrease in heat transfer efficiency can be suppressed. In addition, although the liquid refrigerant introduced into the container flows, since the official groups are disposed separately from each other, the refrigerant becomes easy to flow. Therefore, the contact between the refrigerant liquid and the heat transfer tube can be promoted, and the heat transfer efficiency can be improved. In addition, in the evaporator described above, a plurality of tube groups may be arranged in a staggered manner. A kind of hair dryer ’whose structure is liquid refrigerant is drawn from below the container -5-
裝 訂Binding
k 546459 五、發明説明(3 進,汽化後由上方流出。該蒗發器且 内向上流的傾向。所以在此種^有:狀的冷媒在容器 地被配置,能夠促進朝上為,由於將管群交錯狀 勰品、杳?丨為你* 方流動的冷媒液與傳教管的接 觸,而達到熱傳達效率的提高。 、丹…&的接 此外,至於上述的蒸發罘, 不被配置上述傳熱管的空障:。 、〔的官群裡也可以留置 至於此蒸發器’係由於在管群留置空隙 附近的氣泡變成容易脫離。因 ::中央 的傳熱管影響的氣泡就變少,…:置在…央附近 低。 交乂而旎夠抑制熱傳達效率的降 此外,在上述的此蒗發^ .. ^ …兔裔上述的傳熱管在任何的管群 都可以交錯狀地被棑列。 Μ 如上所述’被引進容器内的液狀冷媒產生流動。所以在 此蒸發器’由於傳熱管也成交錯狀地配置;即使在管群 内,冷媒變成容易流動,而能夠促進冷媒液與傳熱管的接 觸,達到熱傳達效率的提高。 此外,在上述蒸發器,屬於位於上述容器上部的管群的 傳熱官比起位於屬於位於下部的管群的傳熱管可以疏鬆地 被配置。 至於在上述蒸發器,位於容器下部的管群的傳熱管的周 圍所產生的氣泡通過位於上部的管群之時,屬於該的管群 的傳熱管比起下部的管群疏鬆地被配置,氣泡由屬於位於 上方的管群的傳熱管之間變成容易脫離。因此能夠抑制位 於上方的管群的熱傳達效率的降低。 -6- 本紙張尺度適用中國國家標準(CNS) Α4規格(210 X 297公釐)k 546459 V. Description of the invention (3 in, evaporates from above. The hair dryer has a tendency to flow inwardly and upwardly. Therefore, in this case: the shape of the refrigerant is arranged in the container, which can promote upwards. Pipes are staggered, 杳? 丨 for your contact with the refrigerant liquid flowing in the mission tube, and the heat transfer efficiency is improved. Dan ... & In addition, the above-mentioned evaporation 罘 is not configured The above-mentioned obstacles of the heat transfer tube: The [] can also be left in the official group. The evaporator 'is easily detached due to the bubbles near the indwelling gap of the tube group. Because: the bubbles affected by the central heat transfer tube will change. Less,…: placed near… the center is low. It is enough to suppress the decrease in heat transmission efficiency. In addition, the above mentioned ^ .. ^… rabbits. The above heat transfer tubes can be staggered in any group of tubes. The liquid refrigerant introduced into the container flows as described above. Therefore, the evaporators are arranged in a staggered manner because the heat transfer tubes are arranged here; even in the tube group, the refrigerant becomes easy to flow. And can promote refrigerant fluid and The contact of the heat transfer tubes improves the heat transfer efficiency. In addition, in the evaporator, the heat transfer officer belonging to the tube group located in the upper part of the container can be arranged loosely than the heat transfer tubes located in the tube group located in the lower part. As for the above-mentioned evaporator, when the air bubbles generated around the heat transfer tubes of the tube group located at the lower part of the container pass through the tube group located at the upper part, the heat transfer tubes belonging to the tube group are looser than the lower tube group. With the arrangement, the air bubbles are easily separated from the heat transfer tubes belonging to the upper tube group. Therefore, it is possible to suppress the decrease in the heat transfer efficiency of the upper tube group. -6- This paper standard is applicable to the Chinese National Standard (CNS) Α4 standard (210 X 297 mm)
546459 A7 _____ B7 ί、發明説明(4 ) - 有關本發明的冷;東機,其具有一種蒸發^,其係在冷媒 被引進的容器裏,流通被冷卻物的多數傳熱管成摘地被配 置而構成,在上述冷媒與上述被冷卻物進行熱交換,冷卻 該被冷卻物’同時將上述冷媒氣化;以及一種壓縮機:其 係壓縮在該蒸發器被氣化的冷媒;以及一種凝結器,其係 將被壓縮的上述冷媒凝結、液化;還有一種膨服二,其係 在讓液化的上述冷媒流通於上述蒸發器的過程中,將上述 冷媒減壓。 至於此冷凍機,如上所述,能夠提高在蒸發器的傳熱管 的熱傳達效率,其結果是:因為熱交換效率被提高即使抑 制旎源的耗費,能夠得到和先前和同等的性能,尤其是冷 卻效率。 圖面之簡要說明 圖1係表示有關本發明第i實施形態的圖,為冷凍機的概 略圖。 圖2係蒸發器的剖面(在圖1上1卜11剖面)圖。 圖3係表示蒸發器的傳熱管的配置圖。 圖4係表示有關本發明的第2實施形態的蒸發器剖面圖。 圖5係表示有關本發明的第2實施形態的其他例子的蒸發 器剖面圖。 圖6係表示有關本發明的第3實施形態的蒸發器剖面圖。 圖7係表示有關本發明的第4實施形態的蒸發器剖面圖。 圖8係表不有關本發明的其他實施形態的蒸發器剖面圖。 圖9係表示有關本發明的其他實施形態的蒸發器剖面圖。546459 A7 _____ B7. Description of the invention (4)-The cold machine of the present invention has a type of evaporation ^, which is placed in a container where the refrigerant is introduced, and most of the heat transfer tubes that circulate the object to be cooled are cut off. It is configured to perform heat exchange between the refrigerant and the object to be cooled, and to cool the object to be cooled while gasifying the refrigerant; and a compressor that compresses the refrigerant that is vaporized in the evaporator; and a condensation An evaporator is used for condensing and liquefying the compressed refrigerant, and a second type of expansion is for reducing the pressure of the refrigerant during the process of passing the liquefied refrigerant through the evaporator. As for the refrigerator, as described above, the heat transfer efficiency of the heat transfer tube in the evaporator can be improved. As a result, the heat exchange efficiency can be improved, and even if the cost of tritium is suppressed, the same and previous performance can be obtained, especially Is cooling efficiency. Brief Description of the Drawings Fig. 1 is a diagram showing an i-th embodiment of the present invention, and is a schematic diagram of a refrigerator. Fig. 2 is a cross-sectional view of the evaporator (a cross section of Fig. 11 and Fig. 11). Fig. 3 is a layout diagram of a heat transfer tube of an evaporator. Fig. 4 is a sectional view showing an evaporator according to a second embodiment of the present invention. Fig. 5 is a sectional view showing an evaporator according to another example of the second embodiment of the present invention. Fig. 6 is a sectional view showing an evaporator according to a third embodiment of the present invention. Fig. 7 is a sectional view showing an evaporator according to a fourth embodiment of the present invention. Fig. 8 is a sectional view showing an evaporator according to another embodiment of the present invention. Fig. 9 is a sectional view showing an evaporator according to another embodiment of the present invention.
297公釐) 546459 A7 _________B7 五、發明説明(5 ) 圖1 0係為具有冷凍機的習知蒸發器剖面圖。 發明之詳細說明 將有關本發明的蒸發器及冷凍機的第1實施形態表示於圖 1至圖3來說明。 將冷凍機的簡略構成表示於圖丨。於圖所示的冷凍機係具 有在被冷部水與氣體狀的冷媒之間使進行熱交換而將冷媒 凝結、液化的凝結器丨〇,及將凝結的冷媒減壓的膨脹閥 1 1 ’及在凝結的冷媒與冷水(被冷卻物)之間使進行熱交 換,同時將冷媒蒸發、汽化的蒸發器丨2,及將汽化的冷媒 壓縮之後提供給凝結器的壓縮機丨3。在冷凍機内的蒸發器 1 2所製造的冷水係被利用在大樓的空調等等。 条發谷為1 2 ’其構造係在冷媒被引進的圓筒形容器1 4 裏,流通冷水的多數傳熱管成捆地(在圖1有簡略地圖示)被 配置於容器14的長邊方向。傳熱管15與連通於冷水入口 的去程傳熱管及連通於冷水入口 17的回程傳熱管分開,冷 水的方向在連通於冷水入口 16的管路及連通於冷水入口 17 的管路並不相同。 圖2係蒸發器1 2的剖面圖。傳熱管1 5在容器1 4的下半部 被分成A〜I九個管群,該管群a〜I相互相鄰之間並無關 係’並且成父錯狀地被配置。詳細地說就是:管群A〜e被 水平地排列’在其下部,管群F〜I被水平地排列的同時,由 於對管群A〜E橫方向平移所以成交錯狀地被排列。 再者,不管在A〜I任何管群,都聚集有1〇〇根左右的傳熱 管1 5,此外,在這些管群a〜I傳熱管1 5成交錯狀地被排 -8 - 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) M6459 A7 --—-------B7_ 五、發明説明(6 ) ' - 列。此時,也由於在上下多段地被排列的傳熱管丨5在每段 左右地平移’所以成交錯狀地被排列。 、再者,成交錯狀地被排列的傳熱管丨5,如圖3所示其直徑 為D的話,於橫方向相鄰的傳熱管i 5之間的間隔變成 1 . 1 5D 〇 ,至於如上述所構成的蒸發器1 2,由於將傳熱管1 5分成管 群A〜I,管群之間互不相關地被配置,在各管群内的比較 下邊的傳熱管15的周圍所產生的氣泡由管群與管群之間脫 離浮起,存在於管群内的氣泡減少。因此,對配置在管群 中央附近的傳熱管i 5影響的氣泡就變少,而能夠抑制熱傳 達效率的降低。 此外,在谷器1 4内的構造,係液態的冷媒從下部被引 進、、Λ化而從上部流出到容器1 4外,被引進的冷媒在容器 1 4内向上面流動的傾向很強,但是由於管群之間是互不相 關地配置,冷媒變成容易流動。因此,能夠促進冷媒與冷 水的接觸,而達到熱傳達效率的提高。 再者’將管群Α〜I成交錯狀地排列的同時,由於在各管 群A〜I傳熱管1 5也成交錯狀地配置,能夠促進向上方流動 的冷媒液與傳熱管的接觸,而達到熱傳達效率的提高。 如上所述,如果將蒸發器1 2以上述的構造來做的話,能 夠提高熱傳達效率,因此也就能夠提高冷凍機的冷卻效 率。 再者,至於在本實施形態,將傳熱管1 5分成A〜I九個管 群,但是這些按照蒸發器的大小、應該發揮的性能即使分 -9- 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) 546459 A7 B7 五、發明説明(7 ) 為更少數的管群也可以,相反地分為較多的管群也可以。 此外,橫方向相鄰的傳熱管i 5之間的間隔設定為i ·丨5D, 但不限定於此,可以按照各種條件來選擇。 其次,將有關本發明的蒸發器及冷凍機的第2實施形態, 表示於圖4及圖5來說明。在此,對在上述第丨實施形態已 經說明的構成要素付予相同符號,省略說明。 圖4係蒸發器1 2的剖面圖。如圖所示,本實施形態的蒸發 器1 2,在管群A〜E,傳熱管1 5縱橫地被排列成所謂的格子 狀。並且,管群F〜I與上述第i實施形態相同,成交錯狀地 S己置。 再者,在管群A〜E ,橫方向相鄰的傳熱管i 5之間的間隔 被没定為1 . 1 5 D ’傳熱管1 5之間上下的間隔被設定為 2〜3D。此外,在管群F〜I上下方向相鄰的傳熱管Η之間的 間隔比起在管群A〜E的傳熱管L 5上下方向的間隔設定較 窄。也就是說,屬於管群A〜E的傳熱管15比起屬於管群 F〜I的傳熱管1 5排列較疏鬆。 在上述所構成的洛發器12 ’於管群F〜I的傳熱管15周圍 產生的氣泡通過管群A〜E的時候,因為屬於管群a〜E的傳 熱管1 5比起屬於管群F〜I的傳熱管1 5排列較疏鬆,所以, 屬於管群A〜E的傳熱管15之間的氣泡就變成容易脫離,而 能夠抑制熱傳達效率的降低。 如上所述,根據在本實施形態的蒸發器丨2也能夠提高熱 傳達效率,因此,就能夠提高冷凍機的冷卻效率。 再者,在本實施形態,雖然將管群A〜E的傳熱管1 5做成 -10 - 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) 546459 A7 B7297 mm) 546459 A7 _________B7 V. Description of the invention (5) Figure 10 is a sectional view of a conventional evaporator with a refrigerator. DETAILED DESCRIPTION OF THE INVENTION A first embodiment of an evaporator and a refrigerator according to the present invention will be described with reference to Figs. 1 to 3. The schematic structure of a refrigerator is shown in FIG. The refrigerating machine shown in the figure includes a condenser for condensing and liquefying the refrigerant by performing heat exchange between the water in the cooled part and the gaseous refrigerant, and an expansion valve 1 1 ′ for reducing the pressure of the condensed refrigerant. And an evaporator that performs heat exchange between the condensed refrigerant and cold water (the object to be cooled), and at the same time evaporates and vaporizes the refrigerant, and a compressor that provides the condenser with the vaporized refrigerant compressed. The cold water system produced by the evaporator 1 2 in the freezer is used in the air conditioner of the building and the like. The trough is 1 2 '. Its structure is in the cylindrical container 1 4 where the refrigerant is introduced. Most of the heat transfer tubes that circulate cold water are bundled (shown schematically in FIG. 1) and are arranged in the length of the container 14. Side direction. The heat transfer tube 15 is separated from the outbound heat transfer tube connected to the cold water inlet and the return heat transfer tube connected to the cold water inlet 17. The direction of the cold water is in the pipeline connected to the cold water inlet 16 and the pipeline connected to the cold water inlet 17. Not the same. FIG. 2 is a sectional view of the evaporator 12. In the lower half of the container 14, the heat transfer tubes 15 are divided into nine tube groups A to I, and the tube groups a to I are adjacent to each other and are not related, and are arranged in a staggered manner. In detail, the pipe groups A to e are arranged horizontally ', while the pipe groups F to I are arranged horizontally, and the pipe groups A to E are arranged in a staggered manner because they are translated horizontally. In addition, about any of the tube groups A to I, about 100 heat transfer tubes 15 are gathered. In addition, in these tube groups a to I, the heat transfer tubes 15 are arranged in a staggered manner. This paper size applies to the Chinese National Standard (CNS) A4 specification (210 X 297 mm) M6459 A7 ---------- B7_ V. Description of the invention (6) '-column. At this time, the heat transfer tubes 5 arranged in a plurality of stages are also shifted in a staggered manner because they are shifted in each stage. Furthermore, the heat transfer tubes 5 arranged in a staggered pattern, as shown in FIG. 3, having a diameter D, the interval between the heat transfer tubes i 5 adjacent in the horizontal direction becomes 1.1 5D. As for the evaporator 12 constructed as described above, since the heat transfer tubes 15 are divided into tube groups A to I, the tube groups are arranged independently of each other. In each tube group, the heat transfer tubes 15 below are compared. The bubbles generated from the surroundings are separated and floated between the tube group and the tube group, and the air bubbles existing in the tube group are reduced. Therefore, the number of bubbles affecting the heat transfer tube i 5 arranged near the center of the tube group is reduced, and a decrease in heat transfer efficiency can be suppressed. In addition, in the structure of the valley device 14, the liquid refrigerant is introduced from the lower part, and is discharged from the upper part to the outside of the container 14. The introduced refrigerant tends to flow upward in the container 14, but Since the tube groups are arranged independently of each other, the refrigerant becomes easy to flow. Therefore, the contact between the refrigerant and the cold water can be promoted, and heat transfer efficiency can be improved. Furthermore, while the tube groups A to I are arranged in a staggered manner, since the heat transfer tubes 15 are also arranged in a staggered manner in each of the tube groups A to I, the refrigerant liquid flowing upward and the heat transfer tubes can be promoted. Contact, and the heat transfer efficiency is improved. As described above, if the evaporator 12 is configured as described above, the heat transfer efficiency can be improved, and therefore, the cooling efficiency of the refrigerator can be improved. Moreover, in this embodiment, the heat transfer tubes 15 are divided into nine tube groups of A to I, but these are divided into -9 according to the size of the evaporator and the performance that should be exerted. This paper standard applies the Chinese national standard (CNS ) A4 size (210 X 297 mm) 546459 A7 B7 V. Description of the invention (7) It is also possible to have a smaller number of tube groups, and vice versa. In addition, the interval between the heat transfer tubes i 5 adjacent in the horizontal direction is set to i · 5D, but it is not limited to this, and can be selected according to various conditions. Next, a second embodiment of the evaporator and the freezer according to the present invention will be described with reference to FIGS. 4 and 5. Here, the same reference numerals are given to the constituent elements already described in the above-mentioned embodiment, and the description is omitted. Fig. 4 is a sectional view of the evaporator 12; As shown in the figure, in the evaporator 12 according to this embodiment, in the tube groups A to E, the heat transfer tubes 15 are arranged vertically and horizontally in a so-called grid pattern. In addition, the tube groups F to I are the same as the i-th embodiment described above, and they are disposed in a staggered manner. Furthermore, in the tube groups A to E, the interval between the heat transfer tubes i 5 adjacent to each other in the horizontal direction is not set to 1. 1 5 D ', and the interval between the heat transfer tubes 15 and 5 is set to 2 to 3D. . In addition, the interval between the heat transfer tubes 相邻 adjacent in the vertical direction of the tube groups F to I is narrower than the interval in the vertical direction of the heat transfer tubes L 5 in the tube groups A to E. In other words, the heat transfer tubes 15 belonging to the tube groups A to E are arranged looser than the heat transfer tubes 15 belonging to the tube groups F to I. When bubbles formed around the heat transfer tubes 15 of the tube groups F to I pass through the tube groups A to E as described above, the heat transfer tubes 15 belonging to the tube groups a to E belong to The heat transfer tubes 15 of the tube groups F to I are relatively loosely arranged. Therefore, the air bubbles between the heat transfer tubes 15 belonging to the tube groups A to E are easily detached, and a decrease in heat transmission efficiency can be suppressed. As described above, according to the evaporator 2 of this embodiment, the heat transfer efficiency can also be improved, and therefore, the cooling efficiency of the refrigerator can be improved. Moreover, in this embodiment, although the heat transfer tubes 15 of the tube groups A to E are made into -10-this paper size applies the Chinese National Standard (CNS) A4 specification (210 X 297 mm) 546459 A7 B7
格子狀之後,還比管群F〜I的傳熱管丨5排列較疏鬆,但是 將管群A〜E的任何傳熱管1 5或者全體就交錯狀那樣疏鬆2 排列也沒關係。 % & 圖5係表示有關本實施形態的蒸發器丨2的其他例子的剖面 圖。在管群A·〜L’,傳熱管1 5與上述第i的實施形態同樣成 交錯狀地被排列。 至於管群A’〜F,,橫方向相鄰的傳熱管15之間的間隔被 設定為1 · 1 5D。此外,在管群G,〜L,,上下方向相鄰的傳 熱管1 5之間的間隔,比起在管群a,〜F,的傳熱管丨5的上下 方向的間設定置較狹窄。也就是說,屬於管群A,〜F,的傳熱 管1 5比起屬於管群G’〜Lf的傳熱管1 5排列較疏鬆。 如上所述,在配置傳熱管15的蒸發器12,管群A,〜F,及 管群G’〜L1成格子狀地被配置。 根據上述構成,在管群G’〜L’的傳熱管15的周圍產生的 氣泡通過管群A1〜F,的時候,因為這些屬於管群A,〜F,的傳 熱管1 5比起屬於管群G,〜L1的傳熱管1 5配置較疏鬆,所 以,屬於管群A,〜Lf的傳熱管1 5之間的氣泡就變成容易脫 離,而能夠抑制熱傳達效率的降低。因此,能夠提高熱傳 達效率,依此就可以提高冷凍機的冷卻效率。 在上述構成,雖然管群Af〜F’的傳熱管15比起屬於管群 G f〜L '的傳熱管1 5配置較疏鬆,但是將管群a,〜L,的任何 傳熱管1 5或者全體傳熱管1 5就交錯狀那樣疏鬆地配置也可 以。 其次,將有關本發明的蒸發器及冷凍機的第3實施形態表 -11 - 本紙張尺度通用中國國家標準(CNS) A4规格(210 X 297公釐) 546459 A7After the lattice, the heat transfer tubes 5 to 5 of the tube groups F to I are arranged more loosely, but it is also okay to arrange any of the heat transfer tubes 15 or 5 of the tube groups A to E to be loose 2 as a whole. Fig. 5 is a cross-sectional view showing another example of the evaporator 2 according to this embodiment. In the tube groups A · ~ L ', the heat transfer tubes 15 are arranged in a staggered manner similarly to the i-th embodiment. As for the tube groups A 'to F, the interval between the adjacent heat transfer tubes 15 in the horizontal direction is set to 1 · 15D. In addition, the distance between the heat transfer tubes 15 adjacent to each other in the tube group G, ~ L, and the up-down direction is set to be more than that between the heat transfer tubes 15, 5 in the tube group a, ~ F, and narrow. That is, the heat transfer tubes 15 belonging to the tube groups A, ~ F, are arranged more loosely than the heat transfer tubes 15 belonging to the tube group G '~ Lf. As described above, in the evaporator 12 in which the heat transfer tubes 15 are arranged, the tube groups A, to F, and the tube groups G 'to L1 are arranged in a grid pattern. According to the above configuration, when the air bubbles generated around the heat transfer tubes 15 of the tube groups G ′ to L ′ pass through the tube groups A1 to F, because these heat transfer tubes 15 belonging to the tube groups A, to F are compared with The heat transfer tubes 15 belonging to the tube group G to L1 are relatively loosely arranged. Therefore, the air bubbles between the heat transfer tubes 15 belonging to the tube group A to Lf are easily detached, and a reduction in heat transfer efficiency can be suppressed. Therefore, the heat transfer efficiency can be improved, and accordingly, the cooling efficiency of the refrigerator can be improved. In the above configuration, although the heat transfer tubes 15 of the tube group Af to F 'are arranged looser than the heat transfer tubes 15 of the tube group G f to L', any of the heat transfer tubes of the tube group a, ~ L, 15 or the entire heat transfer tubes 15 may be arranged loosely in a staggered manner. Next, the third embodiment of the evaporator and the freezer of the present invention is shown in Table -11-The paper size is in accordance with the Chinese National Standard (CNS) A4 specification (210 X 297 mm) 546459 A7
示於圖6來說明。在此,對 訂於上述各貫她形怨已經說明的 構成要素付予相同符號,省略說明。 圖。6係洛發器! 2的剖面圖。女σ圖所#,在本實施形態的蒸 發器1 2,傳熱官丨5被排在橫方向的4個管群了〜%分開,留 有上:貫穿在各管群之間的空隙。這個空隙,由如先前將 2熱& 1 5父錯狀地配置捆成一捆的情況,從將規定的傳熱 官1 5 一枝或3枝交互拔除地配置,在以下將此當做拔除列 20 〇 再者,在管群J〜Μ,不被配置傳熱管15的空隙與拔除列 2 0平行地被留著。此空隙也同拔除列2 〇從將規定的傳熱管 1 5 —根或二根交互拔除地被留著,所以在以下將此當做輔 助拔除列2 1。 在上述所構成的蒸發器12,由於配置拔除列及輔助拔 除列21,在管群j〜M内的比較的下邊的熱管15周圍產生的 氣泡脫離拔除列2 〇或輔助拔除列2 1浮起。因此,對配置在 官群中央及上方附近的傳熱管1 5影響的氣泡就變少,而能 夠抑制熱傳達效率的降低。 其**人’將有關本發明的蒸發器及冷;東機的第4實施形態表 示於圖7來說明。在此,對於上述各實施形態已經說明的構 成要素付予相同符號,省略說明。 圖7係蒸發器1 2的剖面圖。如圖所示,在本實施形態的蒸 發器12,於管群J,μ,與上述輔助拔除列21不同,上下 沒有脫離的半輔助拔除列2 2與辅助拔除列2 1同樣有被設 置。 -12- 本紙張尺度適用中國國家標準(CNS) Α4規格(210 X 297公釐)This is illustrated in FIG. 6. Here, the same reference numerals are given to the constituent elements that have been described in the above-mentioned respective complaints, and the description is omitted. Illustration. 6 series of locks! Sectional view of 2. Female σ 图 所 #, in the evaporator 12 of this embodiment, the heat transfer officer 5 is divided by 4% in the horizontal direction, leaving a gap between the tube groups. This gap is arranged as a bundle of 2 heat & 1 5 fathers in a staggered arrangement as previously, and a predetermined heat transfer officer 1 5 or 3 branches are removed and arranged alternately, and this will be referred to as the removal row 20 below. 〇 Further, in the tube groups J to M, the gaps in which the heat transfer tubes 15 are not arranged are left in parallel with the removal row 20. This gap is also removed in parallel to the removal of the specified heat transfer tube 15 or two, so the following will be referred to as the auxiliary removal of the removal line 21 in the following. In the evaporator 12 constituted as described above, since the extraction row and the auxiliary extraction row 21 are arranged, bubbles generated around the heat pipe 15 below the comparison in the tube group j to M are separated from the extraction row 2 or the auxiliary extraction row 21 1 floats. . Therefore, the number of bubbles affecting the heat transfer tubes 15 arranged near and above the center of the official group is reduced, and a decrease in heat transfer efficiency can be suppressed. The first person's fourth embodiment of the evaporator and the refrigerator of the present invention is shown in Fig. 7 for explanation. Here, the same reference numerals are given to the constituent elements already described in each of the above embodiments, and the description is omitted. Fig. 7 is a sectional view of the evaporator 12; As shown in the figure, in the vaporizer 12 of this embodiment, the tube group J, µ is different from the above-mentioned auxiliary extraction column 21, and the semi-assisted extraction column 2 2 which is not detached from above and below is provided similarly to the auxiliary extraction column 2 1. -12- This paper size applies to China National Standard (CNS) Α4 size (210 X 297 mm)
裝Hold
線 546459 A7 __B7 五、發明説明(1〇 ) 在上述所構成的蒸發器1 2,由於設置半輔助拔除列2 2, 從管群J,Μ的中央附近的氣泡變成容易脫離,對配置在管 群J,Μ中央及上方附近的傳熱管1 5影響的氣泡變少,因而 能夠抑制熱傳達效率的降低。此外,此半輔助拔除列2 2配 置在管群J〜Μ的任何一個都無妨。 在以下針對其他的實施形態簡單來說明。 圖8係將半辅助拔除列2 2設置於管群j,Μ的下方的例 子。圖9係好像從輔助拔除列2 1將樹枝伸展向斜上方再配 置小的辅助拔除列2 3的例子。這些各種的配置類型,最好 按照蒸發器的大小、應該發揮的性能來選擇。 再者’至於上述各貫施形態的傳熱管1 5,當然能夠使用 渦形管子、鰭狀管及其他一切形態的管材。 此外,至於上述各貫施形態,雖然係以冷水在蒸發器一 個往返的構造為例進行說明,但是有關本發明的蒸發器, 能夠應用於冷水在一個方向流通的,數次往返的,以及從 一邊流入往返後再從另一邊流出的等等所有構造的蒸發器 的技術。Line 546459 A7 __B7 V. Description of the invention (10) In the evaporator 12 constructed as described above, since the semi-assisted removal row 2 2 is provided, the bubbles near the center of the tube group J, M become easy to detach, Since the number of bubbles affected by the heat transfer tubes 15 near the center of the groups J and M is reduced, it is possible to suppress a decrease in heat transmission efficiency. In addition, the semi-assisted removal row 2 2 may be arranged in any one of the pipe groups J to M. Hereinafter, other embodiments will be briefly described. Fig. 8 shows an example in which the semi-assisted removal row 2 2 is provided below the tube group j, M. Fig. 9 shows an example where the branch is extended obliquely upward from the auxiliary removal row 21 and a small auxiliary removal row 23 is arranged. These various configuration types are best selected according to the size of the evaporator and the performance it should play. Furthermore, as for the heat transfer tubes 15 of the above-mentioned various embodiments, of course, scroll tubes, fin tubes, and all other tube materials can be used. In addition, as for each of the above-mentioned embodiments, although the structure in which the cold water flows back and forth in the evaporator is taken as an example, the evaporator of the present invention can be applied to cold water flowing in one direction, several round trips, and from The technology of all the constructed evaporators that flow from one side to the other and then flow out from the other side.
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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JP2000025606A JP3572234B2 (en) | 2000-02-02 | 2000-02-02 | Evaporators and refrigerators |
Publications (1)
Publication Number | Publication Date |
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TW546459B true TW546459B (en) | 2003-08-11 |
Family
ID=29727393
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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TW090118199A TW546459B (en) | 2000-02-02 | 2001-07-25 | Evaporator and refrigerator |
Country Status (3)
Country | Link |
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US (1) | US6497115B1 (en) |
JP (1) | JP3572234B2 (en) |
TW (1) | TW546459B (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3572250B2 (en) * | 2000-10-24 | 2004-09-29 | 三菱重工業株式会社 | Condenser for refrigerator |
DE202010014128U1 (en) * | 2010-10-12 | 2011-02-24 | Tranter Pressko Gmbh | Assembly of heat exchanger and liquid separator |
JP5777370B2 (en) * | 2011-03-30 | 2015-09-09 | 三菱重工業株式会社 | Reboiler |
CN103958996B (en) * | 2011-09-26 | 2016-06-08 | 特灵国际有限公司 | Refrigerant processes in HVAC system |
JP6423221B2 (en) * | 2014-09-25 | 2018-11-14 | 三菱重工サーマルシステムズ株式会社 | Evaporator and refrigerator |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1562682A (en) * | 1921-06-29 | 1925-11-24 | Carl F Braun | Condenser |
US2254189A (en) * | 1940-03-07 | 1941-08-26 | Lummus Co | Heat exchanger |
US2964926A (en) * | 1958-10-17 | 1960-12-20 | Trane Co | Flooded water chiller |
US2995341A (en) * | 1959-01-08 | 1961-08-08 | Griscom Russell Co | Feed water heater sub-cooling zone |
US3191396A (en) * | 1963-01-14 | 1965-06-29 | Carrier Corp | Refrigeration system and apparatus for operation at low loads |
US3191674A (en) * | 1963-06-18 | 1965-06-29 | Westinghouse Electric Corp | Shell-and-tube type heat exchangers |
US3250084A (en) * | 1963-09-25 | 1966-05-10 | Carrier Corp | Control systems |
US3242689A (en) * | 1964-03-13 | 1966-03-29 | Worthington Corp | Cooling system and apparatus |
US3257817A (en) * | 1964-07-28 | 1966-06-28 | Carrier Corp | Refrigeration apparatus and method |
US3267693A (en) | 1965-06-29 | 1966-08-23 | Westinghouse Electric Corp | Shell-and-tube type liquid chillers |
US3587732A (en) * | 1969-08-14 | 1971-06-28 | Olin Mathieson | Heat exchanger formed by modules |
JPS61262567A (en) | 1985-05-17 | 1986-11-20 | 株式会社荏原製作所 | Evaporator for refrigerator |
US4843837A (en) | 1986-02-25 | 1989-07-04 | Technology Research Association Of Super Heat Pump Energy Accumulation System | Heat pump system |
US6161613A (en) | 1996-11-21 | 2000-12-19 | Carrier Corporation | Low pressure drop heat exchanger |
-
2000
- 2000-02-02 JP JP2000025606A patent/JP3572234B2/en not_active Expired - Lifetime
-
2001
- 2001-07-23 US US09/910,072 patent/US6497115B1/en not_active Expired - Lifetime
- 2001-07-25 TW TW090118199A patent/TW546459B/en not_active IP Right Cessation
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US6497115B1 (en) | 2002-12-24 |
JP3572234B2 (en) | 2004-09-29 |
JP2001215070A (en) | 2001-08-10 |
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